Center for Hydrate Research, Department of Chemical and Biological Engineering, Colorado School of Mines , Golden, Colorado 80401, United States.
Faculty of Chemical & Natural Resources Engineering, Universiti Malaysia Pahang , Lebuhraya Tun Razak, 26300 Gambang, Malaysia.
Langmuir. 2017 Oct 24;33(42):11436-11445. doi: 10.1021/acs.langmuir.7b02642. Epub 2017 Oct 3.
In situ rheological measurements for clathrate hydrate slurries were performed using a high pressure rheometer to determine the effect of hydrate particles on the viscosity and transportability of these slurries. These measurements were conducted using a well-characterized model water-in-oil emulsion ( Delgado-Linares et al. Model Water in-Oil Emulsions for Gas Hydrate Studies in Oil Continuous Systems . Energy Fuels 2013 , 27 , 4564 - 4573 ). The emulsion consists of a model liquid hydrocarbon, water, and a surfactant mixture of sorbitane monooleate 80 (Span 80) and sodium di-2-ethylhexylsulfosuccinate (Aerosol OT, AOT). This emulsion was used as an analog to water-in-crude oil (w/o) emulsions and provides reproducible results. The flow properties of the model w/o emulsion prior to hydrate formation were investigated in terms of several parameters including water percentage, temperature and pressure. A general equation that describes the viscosity of the emulsion as a function of the aforementioned parameters was developed. This general equation was able to predict the viscosity of a saturated emulsion at various temperatures and water percentages to within ±13% error. The general equation was then used to analyze the effect of hydrate formation on the transportability of gas hydrate slurries. As for hydrate slurries investigation, measurements were performed using methane gas as the hydrate former and a straight vane impeller as a stirring system. Tests were conducted at constant temperature and pressure (1 °C and 1500 psig of methane) and water percentages ranging from 5 to 30 vol %. Results of this work were analyzed and presented in terms of relative values, i.e., viscosities of the slurries relative to the viscosities of the continuous phase at similar temperature and pressure. In this work, a correlation to predict the relative viscosity of a hydrate slurry at various hydrate volume fractions was developed. Analysis of the developed correlation showed that the model was able to predict the relative viscosity of a hydrate slurry to within ±17% error.
采用高压流变仪对笼形水合物浆料进行了原位流变测量,以确定水合物颗粒对这些浆料的粘度和可输送性的影响。这些测量是使用一种经过良好表征的模型油包水乳状液(Delgado-Linares 等人,Model Water in-Oil Emulsions for Gas Hydrate Studies in Oil Continuous Systems,Energy Fuels,2013 年,27 卷,4564-4573)进行的。乳状液由模型液态烃、水和山梨糖醇单油酸酯 80(Span 80)和二-2-乙基己基磺基琥珀酸钠(Aerosol OT,AOT)的表面活性剂混合物组成。该乳液用作水在原油(w/o)乳液的模拟物,并提供可重复的结果。在水合物形成之前,根据几个参数,包括水的百分比、温度和压力,研究了模型 w/o 乳液的流动特性。开发了一个描述乳液粘度作为上述参数函数的通用方程。该通用方程能够在±13%的误差范围内预测不同温度和水百分比下饱和乳液的粘度。然后,使用该通用方程分析水合物形成对气体水合物浆料可输送性的影响。对于水合物浆料的研究,使用甲烷作为水合物形成剂,直叶片搅拌器作为搅拌系统进行测量。在恒定温度和压力(1°C 和 1500 psig 的甲烷)以及水的百分比范围为 5 到 30 体积%的条件下进行了测试。对这些工作的结果进行了分析,并以相对值表示,即类似温度和压力下浆料的粘度与连续相的粘度之比。在这项工作中,开发了一个预测各种水合物体积分数下水合物浆料相对粘度的相关性。对开发的相关性的分析表明,该模型能够在±17%的误差范围内预测水合物浆料的相对粘度。